EP2171787A1 - Apparatus for recirculation of a cathode gas in a fuel cell arrangement, method for shutting down a fuel cell apparatus with the fuel cell arrangement - Google Patents
Apparatus for recirculation of a cathode gas in a fuel cell arrangement, method for shutting down a fuel cell apparatus with the fuel cell arrangementInfo
- Publication number
- EP2171787A1 EP2171787A1 EP08773516A EP08773516A EP2171787A1 EP 2171787 A1 EP2171787 A1 EP 2171787A1 EP 08773516 A EP08773516 A EP 08773516A EP 08773516 A EP08773516 A EP 08773516A EP 2171787 A1 EP2171787 A1 EP 2171787A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- cathode gas
- fuel cell
- cathode
- recirculation
- partially consumed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
- H01M8/04746—Pressure; Flow
- H01M8/04753—Pressure; Flow of fuel cell reactants
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04197—Preventing means for fuel crossover
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04223—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
- H01M8/04231—Purging of the reactants
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M2008/1095—Fuel cells with polymeric electrolytes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
- H01M8/04097—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with recycling of the reactants
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04313—Processes for controlling fuel cells or fuel cell systems characterised by the detection or assessment of variables; characterised by the detection or assessment of failure or abnormal function
- H01M8/0444—Concentration; Density
- H01M8/0447—Concentration; Density of cathode exhausts
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Definitions
- Apparatus for recirculation of a cathode gas in a fuel cell arrangement method for shutting down a fuel cell apparatus with the fuel cell arrangement
- the invention relates to an apparatus for recirculation of a cathode gas in a fuel cell arrangement having a cathode gas supply for supplying the cathode gas to a cathode area in the fuel cell arrangement, having a cathode gas outlet for carrying the partially consumed cathode gas out of the cathode area, and having a recirculation guide for recirculation of the partially consumed cathode gas from a junction point in the cathode gas outlet into a supply point in the cathode gas supply, and to a method for shutting down a fuel cell apparatus which is formed from the apparatus and the fuel cell arrangement.
- Fuel cell apparatuses are used to convert chemical energy to electrical energy, with a fuel, for example hydrogen, being reacted with an oxidant, for example environmental air, in an electrochemical process.
- Fuel cell apparatuses such as these are on the one hand used in a stationary form, and on the other hand, as mobile generators, they provide the capability to supply power to a drive train in a vehicle.
- the document DE 102 03 029 Al discloses a fuel cell apparatus having a specific configuration of an apparatus for supplying a medium containing oxygen into a cathode area of a fuel cell in the fuel cell apparatus.
- cathode gas which has been partially consumed in the electrochemical process be recirculated, starting from a cathode outlet, be mixed with fresh cathode gas and then be supplied to the cathode input again.
- the particular advantages of this procedure are that the water which is created during the electrochemical process is fed back through the partially consumed cathode gas and is used to moisturize the sensitive intermediate membrane between the cathode area and the anode area.
- a controllable restriction apparatus is arranged in a recirculation line, in order to control the proportion of the recirculated, partially consumed cathode gas.
- Laid-Open Specification DE 102 047 87 Al relates to a flap valve for fuel sets, which is intended to be used in particular in the field of fuel supply, that is to say in the anode gas circuit.
- the flap valve comprises a flap which is arranged within a flow channel and can be pivoted via a moveable shaft, and a seal which is connected to a channel wall and has a so-called pressure pocket.
- valve apparatus in the form of a bypass valve is known from the document DE 103 25 196 B3, which is in the form of a switching flap and has a flap plate which can be pivoted by means of a shaft which is arranged outside the flap plate.
- a sealing element is provided, which is arranged on the circumference of the flap plate and has at least two sealing lips which run parallel to one another.
- the field of the application is considered to be fuel cell apparatuses, in particular in the area of the anode gas circuit.
- Laid-Open Specification DE 103 28 246 Al relates to a further valve which has a valve body which is mounted by means of a shaft that is passed through.
- a sealing column is fitted on the valve body in order to seal the shaft, as well as a sealing strip which runs around the edge of the circumference, with the sealing strip being interrupted in the circumferential direction in order to allow the shaft to pass through, and to allow the sealing column to be attached.
- the fuel cell apparatus according to the document DE 102 03 029 Al is regarded as the closest prior art.
- the invention is based on the object of providing an apparatus for recirculation of a cathode gas in a fuel cell arrangement, which apparatus allows the fuel cell arrangement to be shut down safely, and of proposing a corresponding method for shutting down a fuel cell apparatus which is formed from the apparatus and the fuel cell arrangement.
- an apparatus for recirculation of a cathode gas in a fuel cell arrangement, which apparatus is probably suitable and/or designed for use as a mobile energy source, in particular in a vehicle.
- the fuel cell arrangement preferably has a multiplicity of fuel cells, in particular more than 100, which are connected in series, for example, in order to produce an adequate output voltage.
- the fuel cells each have a cathode area and an anode area which are separated from one another by a proton exchange membrane.
- the totality of the cathode areas and of the anode areas, respectively, is referred to in brief in the following text as the cathode area and anode area respectively.
- the apparatus has a cathode gas supply for supplying the cathode gas, in particular oxygen or environmental air, to the cathode area in the fuel cell arrangement and, for example, is in the form of a supply line or a tube.
- a cathode gas supply for supplying the cathode gas, in particular oxygen or environmental air, to the cathode area in the fuel cell arrangement and, for example, is in the form of a supply line or a tube.
- the apparatus For carrying the partially consumed cathode gas out of the cathode area, the apparatus has a cathode gas outlet which, for example, is also in the form of a line or a tube.
- the apparatus has a recirculation guide for recirculation of the partially consumed cathode gas from a junction point in the cathode gas outlet into a supply point in the cathode gas supply.
- the cathode gas outlet is therefore split at a junction point in the flow direction downstream from the cathode area, with a first flow element being emitted, for example, into the environment and a second flow element being passed via the recirculation guide to the supply point in the cathode gas supply.
- the partially consumed cathode gas is mixed with fresh cathode gas, for example from the environment, at the supply point, and is passed to the cathode area again.
- a blocking apparatus which is designed to block the cathode gas supply in a gas- tight manner upstream of the supply point and to block the cathode gas outlet downstream from the junction point.
- a closed circuit for the partially consumed cathode gas is formed when the blocking apparatus is closed, with the partially consumed cathode gas being passed from the cathode area via the junction point and via the supply point into the cathode area again, with no fresh cathode gas being added.
- This measure and the procedure result in the oxygen being extracted from the cathode area and from the cathode gas system, thus preventing or at least reducing the corrosion processes associated with it.
- a further possible advantage is that no oxygen or little oxygen can diffuse into the anode area during the rest phase of the fuel cell arrangement, therefore in this way also making it possible to effectively prevent corrosion processes in the anode area of the fuel cell arrangement while it is shut down.
- the apparatus has a continuous-flow machine which is designed to recirculate the partially consumed cathode gas when the blocking apparatus is closed.
- the continuous-flow machine is therefore arranged and/or connected for flow purposes such that it can move the partially consumed cathode gas in the closed circuit for the partially consumed cathode gas.
- the continuous-flow machine is preferably also designed to compress the cathode gas when the blocking apparatus is open, so that it carries out a dual function, therefore saving components .
- the continuous-flow machine is intended to be a turbocharger (ETC) which is or can be electrically driven, although it may also be in the form of a volumetric compressor, for example a screw-type compressor or Roots compressor.
- ETC turbocharger
- this may also relate to an impulse exchange machine.
- This embodiment once again underscores the inventive concept of circulating the partially consumed cathode gas when the blocking apparatus is closed, in order to reduce oxygen content.
- the apparatus has a control apparatus, which is in the form of programming and/or circuitry, and is designed to block the blocking apparatus and at the same time to activate the continuous-flow machine, or to keep it activated in a switched-off operating mode. It is also possible for the switched-off operating mode to occur in the course of maintenance, repair or the like.
- the control apparatus may be in the form of a local control or a part of a higher-level control system.
- the control apparatus preferably allows a plurality of operating modes, with the switched-off operating mode representing one possible operating mode.
- the control apparatus is preferably in the form of programming and/or circuitry such that the switched-off operating mode is maintained for a defined time interval and/or as a function of the remaining oxygen content in the partially consumed cathode gas.
- a time interval determined and/or calculated from an empirical value is entered by a user for a defined time interval.
- appropriate sensors in particular oxygen sensors, are provided in the apparatus for closed-loop or open-loop control as a function of the remaining oxygen content in the partially consumed cathode gas, with the recirculation being deactivated when a limit value is undershot.
- the voltage of the fuel cell can also be used as a switch-off criterion since, when no oxygen is present, no voltage is produced either.
- the blocking apparatus comprises one or more valves or restrictors which is or are designed and/or arranged in order to block the cathode gas outlet and/or the cathode gas supply.
- the valves may be designed, for example, as in the initially cited documents DE 102 047 87 Al, DE 103 25 196 B3 or DE 103 28 246 Al, whose disclosure content relating to the physical form is hereby included in its entirety in the present disclosure, by reference .
- valve or valves and/or the restrictor or restrictors are/is designed to be self-latching, in particular self-latching in the open and/or closed state.
- the valves and/or restrictors it is in this case preferable for the valves and/or restrictors to be open when no current is applied to an operation and to be closed when no current is flowing after the fuel cell arrangement has been switched off, in order to prevent the ingress of fresh cathode gas or environmental air.
- One possible implementation of the self- latching valves or restrictors is for these devices to be driven via a worm drive, in particular a self-locking worm drive .
- valves and/or restrictors of the blocking apparatus preferably be driven by a common actuator. This can be achieved, for example, by means of a linkage or a common shaft or a Bowden cable, in order to mechanically couple the valves and restrictors.
- each valve and each restrictor can also be allocated a separate actuator.
- At least one of the restrictors in the blocking apparatus preferably has a restrictor valve and optionally a restrictor valve housing, with the restrictor valve being sealed with respect to the restrictor valve housing and the gas-carrying lines by means of an elastic sealing system.
- the restrictor it is possible to seal the restrictor by means of a circumferential seal on a sealing disc of the restrictor valve and/or for the restrictor valve housing to be rubber- coated internally, in particular in those areas on which the restrictor valve rests in the closed state.
- a modification of the invention proposes that the blocking apparatus has a pressure maintenance mechanism, in particular a pressure maintenance valve, preferably in the form of a restrictor or control valve and/or a proportional valve, which carries out the function of blocking the cathode gas outlet.
- a pressure maintenance mechanism in particular a pressure maintenance valve, preferably in the form of a restrictor or control valve and/or a proportional valve, which carries out the function of blocking the cathode gas outlet.
- a pressure maintenance mechanism which already exists on the cathode outlet side in the fuel cell apparatus to be modified in a simple manner in order to integrate the additional functionality of blocking the gas flow.
- only one blocking device is required to block the cathode gas supply.
- a further subject matter of the invention relates to a fuel cell apparatus designed in particular for a vehicle, which apparatus comprises the fuel cell arrangement and the apparatus for recirculation according to one of the preceding claims and/or as has been described above.
- a next subject matter of the invention relates to a method for switching off or shutting down a fuel cell apparatus according to Claim 14, with, when the fuel cell apparatus is being switched off, the blocking apparatus being switched such that the partially consumed gas circulates in a closed circuit through the cathode area.
- the partially consumed cathode gas is preferably circulated until the oxygen in the cathode gas is consumed, or has fallen below a limit value.
- Figure 1 shows a schematic block diagram of a fuel cell apparatus, as a first exemplary embodiment of the invention.
- Figure 1 shows a schematic illustration of a fuel cell apparatus 1 having an apparatus for recirculation 2 as one exemplary embodiment of the invention.
- the fuel cell apparatus 1 comprises a fuel cell stack 3 which has a plurality of fuel cells, but at least one fuel cell.
- the fuel cell stack 3 comprises an anode area 4 and a cathode area 5, which are separated from one another by means of a membrane 6 (PEM) .
- PEM membrane 6
- the fuel cell apparatus 1 has a cathode gas supply 7 whose input is connected to the environment or to an oxygen tank, and whose output opens in the cathode area 5. Originating from the environment or the oxygen tank, an oxidant mass flow is passed via the cathode gas supply 7 into the cathode area 5, in order to carry out an electrochemical reaction there, in a known manner, with a fuel in the anode area 4 in order to produce electrical energy.
- a compressor 8 is arranged in the cathode gas supply 7 in order to compress the supplied gas, and is in the form of a volumetric or impulse exchange machine, but particularly preferably a continuous-flow machine (turbocharger or turbocompressor) .
- the gas is compressed using the dynamic princip Ie, in which energy transmission preferably takes place via an impeller with blades, through which flow passes continuously.
- the partially consumed cathode gas which is carried out of the cathode area 5 after the electrochemical reaction is at least partially dissipated into the environment via a cathode gas outlet 9 originating from the cathode area 5.
- the outlet line 9 has a junction point 10 downstream from the cathode area 5, to which junction point 10 a recirculation guide 11 is connected.
- the recirculation guide 11 connects the junction point 10 to a supply point 12 in the cathode gas supply 7.
- the supply point 12 is arranged upstream from the continuous-flow machine 8 in the flow direction, that is to say on the suction side of the continuous-flow machine.
- a portion of the partially consumed cathode gas is therefore tapped off through the recirculation guide 11 and is added to the fresh cathode gas fl ow, with this mixture being compressed as the working gas in the continuous-flow machine 8 and finally being supplied to the cathode area 5.
- the recirculation guide 11 is provided with closed-loop or open- loop control via a valve 13 as a function of the required moisture or the mass flow of the oxidant, for example, the recirculation apparatus 2 is switched when the fuel cell apparatus 1 is being shut down or switched off such that the partially consumed cathode gas is circulated in a closed circuit through the cathode area 5 without fresh cathode gas being supplied, in order to completely or virtually completely dissipate the oxygen remaining in the partially consumed cathode gas .
- the fuel cell apparatus 1 has a control apparatus 14 which is designed to control an input restrictor 15 and an output restrictor 16, as well as the continuous-flow machine 8.
- the input restrictor 15 is arranged in the flow upstream of the supply point 12 in the cathode gas supply 7 and makes it possible to block the cathode gas supply 7 in a gas-tight manner such that no fresh cathode gas can be supplied in the direction of the cathode area 5.
- the output restrictor 16 is arranged in the flow downstream from the junction point 10 and allows the cathode gas outlet to be blocked in a gas- tight manner, so that no fresh cathode gas or environmental air can enter in the direction of the cathode area 5 from this side either.
- the input and/or output restrictors 15, 16 each, for example, have a restrictor valve which is provided with an elastic seal which ensures adequate, gas-tight sealing of the components.
- a restrictor valve which is provided with an elastic seal which ensures adequate, gas-tight sealing of the components.
- one such restrictor valve has a circumferential seal.
- the input and/or output restrictors 15, 16 have a restrictor valve housing which is provided with a rubber coating for sealing purposes in the contact area with the restrictor valve.
- Each of the restrictors 15, 16 may have its own actuator for drive purposes, or alternatively and advantageously a common actuator can be provided for control purposes - since these two restrictors are each switched at the same time - and passes the control movements to the restrictors 15, 16 by cables, linkages or the like.
- the control apparatus 14 closes the input restrictor 15 and the output restrictor 16 and activates the continuous-flow machine 8, resulting in recirculation of the partially consumed cathode gas via the cathode area 5 and the recirculation guide 11. This recirculation is continued until the oxygen in the partially consumed cathode or recirculation gas has been adequately dissipated by electrochemical or catalytic processes. The control apparatus 14 then switches off the continuous-flow machine 8.
- This switching-off procedure ensures that no oxygen or only a small residual amount of oxygen remains in the cathode-side area of the fuel cell apparatus 1. Furthermore, this ensures that no oxygen can diffuse from the cathode area 5 into the anode area 4, thus also resulting in an oxygen-free or low- oxygen area there. In consequence, the fuel cell apparatus 1 is switched by the proposed apparatus and the proposed method to have little or no oxygen, so that corrosion processes are prevented, or are at least greatly slowed down, and the life of the fuel cell apparatus 1 and in particular of the membrane 6 can be considerably lengthened.
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102007035056A DE102007035056A1 (en) | 2007-07-26 | 2007-07-26 | A device for recirculating a cathode gas in a fuel cell assembly, a method of shutting down a fuel cell device with the fuel cell assembly |
PCT/EP2008/004931 WO2009012854A1 (en) | 2007-07-26 | 2008-06-19 | Apparatus for recirculation of a cathode gas in a fuel cell arrangement, method for shutting down a fuel cell apparatus with the fuel cell arrangement |
Publications (1)
Publication Number | Publication Date |
---|---|
EP2171787A1 true EP2171787A1 (en) | 2010-04-07 |
Family
ID=39736993
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP08773516A Withdrawn EP2171787A1 (en) | 2007-07-26 | 2008-06-19 | Apparatus for recirculation of a cathode gas in a fuel cell arrangement, method for shutting down a fuel cell apparatus with the fuel cell arrangement |
Country Status (5)
Country | Link |
---|---|
US (1) | US8691452B2 (en) |
EP (1) | EP2171787A1 (en) |
JP (1) | JP2010534902A (en) |
DE (1) | DE102007035056A1 (en) |
WO (1) | WO2009012854A1 (en) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2961959B1 (en) * | 2010-06-29 | 2013-01-25 | Michelin Soc Tech | POWER-ENGINE AND FUEL CELL VEHICLE HAVING A SODIUM CHLORATE DECOMPOSITION REACTOR FOR SUPPLYING THE OXYGEN CELL |
CN105556724B (en) | 2013-05-24 | 2018-03-23 | 水吉能公司 | System and method for controlling fuel battery voltage |
EP2840636A1 (en) * | 2013-08-20 | 2015-02-25 | Siemens Aktiengesellschaft | Method for operating a fuel cell stack and fuel cell stack and fuel cell system |
GB2510256A (en) * | 2013-12-19 | 2014-07-30 | Daimler Ag | Fuel cell system and method for operating a fuel cell system |
US9806356B2 (en) * | 2014-09-24 | 2017-10-31 | GM Global Technology Operations LLC | Systems and methods for controlling oxygen concentration in a cathode of a fuel cell system |
DE102016003795A1 (en) | 2016-03-26 | 2017-09-28 | Daimler Ag | Device for supplying air to a fuel cell |
DE102019218822A1 (en) * | 2019-12-04 | 2021-06-10 | Robert Bosch Gmbh | Fuel cell system to ensure sustainable and energy-efficient operation |
DE102022201540A1 (en) | 2022-02-15 | 2023-08-17 | Robert Bosch Gesellschaft mit beschränkter Haftung | Athode path for a fuel cell system, fuel cell system and method for operating a fuel cell system |
Family Cites Families (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001006707A (en) * | 1999-06-17 | 2001-01-12 | Aisin Seiki Co Ltd | Fuel cell system |
JP2001006697A (en) * | 1999-06-23 | 2001-01-12 | Daihatsu Motor Co Ltd | Fuel cell and fuel cell system |
JP4809965B2 (en) * | 2000-01-28 | 2011-11-09 | 本田技研工業株式会社 | Hydrogen supply system for hydrogen fueled devices and electric vehicles |
JP2002156057A (en) * | 2000-11-20 | 2002-05-31 | Denso Corp | Flow control valve and fuel cell system using the same |
US6797027B2 (en) * | 2001-04-11 | 2004-09-28 | Donaldson Company, Inc. | Filter assemblies and systems for intake air for fuel cells |
US6780534B2 (en) * | 2001-04-11 | 2004-08-24 | Donaldson Company, Inc. | Filter assembly for intake air of fuel cell |
JP2003042330A (en) * | 2001-07-25 | 2003-02-13 | Saginomiya Seisakusho Inc | Driving device for fluid control valve, and fuel cell power generating device |
DE10203029A1 (en) | 2002-01-26 | 2003-07-31 | Ballard Power Systems | Arrangement for feeding medium with oxygen to fuel cell cathode chamber feeds back medium mixture from cathode chamber via choke device into medium upstream of transport device |
DE10204787A1 (en) | 2002-02-06 | 2003-08-21 | Pierburg Gmbh | Flap valve for fuel units |
JP2004022487A (en) * | 2002-06-20 | 2004-01-22 | Nissan Motor Co Ltd | Fuel cell system |
DE10325196B8 (en) | 2003-06-04 | 2005-06-30 | Pierburg Gmbh | bypass valve |
DE10328246B4 (en) | 2003-06-24 | 2007-04-26 | Pierburg Gmbh | Automotive valve |
US6984464B2 (en) * | 2003-08-06 | 2006-01-10 | Utc Fuel Cells, Llc | Hydrogen passivation shut down system for a fuel cell power plant |
JP2005100846A (en) | 2003-09-25 | 2005-04-14 | Nissan Motor Co Ltd | Fuel cell system |
JP3889002B2 (en) | 2004-01-07 | 2007-03-07 | 松下電器産業株式会社 | Fuel cell |
JP4634085B2 (en) | 2004-07-15 | 2011-02-16 | 日本電産サンキョー株式会社 | Multi-channel pump, fuel cell and control method thereof |
JP2006185904A (en) * | 2004-11-30 | 2006-07-13 | Nissan Motor Co Ltd | Fuel cell system |
JP4728686B2 (en) * | 2005-04-20 | 2011-07-20 | アイシン精機株式会社 | Fuel cell system |
JP2007005170A (en) * | 2005-06-24 | 2007-01-11 | Nissan Motor Co Ltd | Fuel cell system |
JP2007078028A (en) * | 2005-09-12 | 2007-03-29 | Star Micronics Co Ltd | Valve gear |
US20070087233A1 (en) | 2005-10-12 | 2007-04-19 | Janusz Blaszczyk | System and method of controlling fuel cell shutdown |
JP2007123013A (en) * | 2005-10-27 | 2007-05-17 | Nissan Motor Co Ltd | Fuel cell system |
US20070154752A1 (en) | 2005-12-29 | 2007-07-05 | Mcelroy James F | Starting up and shutting down a fuel cell stack |
US20080053808A1 (en) * | 2006-08-29 | 2008-03-06 | Peffley Thomas R | Spring return worm gear drive actuator and method |
US20080187788A1 (en) * | 2007-02-06 | 2008-08-07 | Fellows Richard G | System and method of operation of a fuel cell system and of ceasing the same for inhibiting corrosion |
-
2007
- 2007-07-26 DE DE102007035056A patent/DE102007035056A1/en not_active Withdrawn
-
2008
- 2008-06-19 WO PCT/EP2008/004931 patent/WO2009012854A1/en active Application Filing
- 2008-06-19 JP JP2010517282A patent/JP2010534902A/en active Pending
- 2008-06-19 US US12/670,824 patent/US8691452B2/en not_active Expired - Fee Related
- 2008-06-19 EP EP08773516A patent/EP2171787A1/en not_active Withdrawn
Also Published As
Publication number | Publication date |
---|---|
DE102007035056A1 (en) | 2009-01-29 |
JP2010534902A (en) | 2010-11-11 |
WO2009012854A1 (en) | 2009-01-29 |
US8691452B2 (en) | 2014-04-08 |
US20110045368A1 (en) | 2011-02-24 |
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